JP2009127060A - Production method of cold-rolled steel sheet - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To stably produce a cold-rolled steel sheet with high flatness comprising e.g. a high-tensile material by inhibiting occurrence of temperature unevenness in the width direction of a strip, which is caused by e.g. dripping down water contained in mist sprayed onto the strip, on a surface of the strip in a cooling zone in a continuous annealing furnace wherein the strip is continuously annealed while being continuously conveyed in the vertical direction. <P>SOLUTION: The cold-rolled steel sheet is produced by continuously cooling and annealing the strip by spraying the mist containing water onto the heated strip continuously conveyed in the vertical direction in the continuous annealing furnace. When the strip temperature is above 400°C, the water temperature is adjusted to ≤45°C, and when the strip temperature is 200-400°C, the water temperature is adjusted to ≥40°C. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a method of manufacturing a cold-rolled steel sheet, and specifically, is included in mist sprayed on a strip in a cooling zone in a continuous annealing furnace that performs annealing while continuously conveying a heated strip in the vertical direction. The present invention relates to a method for stably producing a cold-rolled steel sheet having a good flatness made of, for example, a high-tensile material by suppressing the occurrence of temperature unevenness in the width direction of the strip due to water dripping down the surface of the strip. .

  As is well known, the mechanical properties of high-strength steel plates, in particular, are determined by heating and soaking using a vertical continuous annealing furnace that continuously anneals by heating, soaking and cooling while conveying the strip in the vertical direction. This is ensured by rapid cooling and tissue control.

  In this cooling, a mist in which gas and water are mixed or a water spray is generally used in combination as a cooling medium for the strip. If the amount of water contained in the mist is increased in order to increase the cooling capacity and cool at a sufficient cooling rate, water flowing down the surface of the strip conveyed in the vertical direction (hereinafter referred to as “dripping water” in this specification). ”) Will inevitably increase. And since this water also cools the strip, temperature unevenness in the width direction of the strip occurs, thereby causing variations in the mechanical properties of the high-tensile steel sheet to be manufactured and defects in flatness. If variations occur due to mechanical properties, for example, when pressing with this high-tensile steel sheet as a raw material, shape defects or insufficient product performance may occur. On the other hand, if flatness defects occur, the product cannot be shipped as a yield. Decreases.

  In order to prevent the occurrence of such a problem, Patent Document 1 discloses that when the temperature of the strip is lowered to a temperature 100 ° C. higher than 350 to 500 ° C., which is the winding temperature of the strip (cooling stop temperature). By spraying and cooling a mist containing water at 45 to 60 ° C., thereby extending the duration of film boiling in which heat transfer is performed through a vapor film formed between the strip and water. By suppressing the occurrence of transition and nucleate boiling by lowering the transition temperature (quenching start point temperature) that changes from boiling to nucleate boiling where heat is transferred when bubbles come into direct contact with the strip An invention for manufacturing a hot-rolled steel sheet by reducing the temperature deviation inside the strip is disclosed.

Patent Document 2 discloses an invention in which a metal strip is mist-cooled with film boiling without causing transition boiling by appropriately controlling the water density of the mist sprayed on the strip.
Japanese Patent Laid-Open No. 06-256858 JP 2000-178658 A

  In the invention disclosed in Patent Document 1, there is a possibility that the cooling rate applied to the strip is lowered, and a hot-rolled steel sheet having a desired high strength cannot be manufactured. Also, if the amount of water contained in the mist is increased to increase the cooling capacity, the convection water on the surface of the strip increases, and the temperature unevenness in the width direction of the strip increases rapidly, resulting in poor strip flatness. And cause variation in mechanical properties.

  In the invention disclosed in Patent Document 2, the whole is weakly cooled, and the necessary mechanical properties of the steel sheet cannot be obtained. In order to increase the strength, it is sufficient to increase the content of the alloy element in the strip, but this increases the cost of the product. Further, if the mist water density is increased immediately after the start of cooling when the strip temperature is high and strong cooling is performed, the amount of dripping water increases and the temperature unevenness in the width direction of the strip increases. Variations due to characteristic parts and poor flatness occur.

  In this way, the mechanical properties of the cold-rolled steel sheet can be controlled by rapidly cooling and microstructure control by spraying mist after heating and soaking in a vertical continuous annealing furnace in which the strip is continuously passed in the vertical direction. If the amount of water contained in the mist is increased in order to increase the cooling capacity and sufficiently cool when securing the width of the strip in the conventional invention, the drooping water on the surface of the strip increases. It was inevitable that temperature unevenness in the direction occurred, resulting in fluctuations in mechanical properties and poor flatness of the steel sheet to be produced.

  The present invention manufactures a cold-rolled steel sheet by continuously cooling and heat-treating this strip by spraying water-containing mist or water onto a heated strip that is continuously conveyed in the vertical direction. When the strip temperature is over 400 ° C., the water temperature is 45 ° C. or lower, and when the strip temperature is 400 ° C. or lower and 200 ° C. or higher, the water temperature is 40 ° C. or higher. It is a manufacturing method of the cold-rolled steel sheet characterized by these.

In the method for manufacturing a cold-rolled steel sheet according to the present invention, it is desirable that the total amount of water sprayed on the strip is 500 (L / m ² ) / min or less in terms of the average water density at the water jet collision point. . In this invention, the “jet collision point” means a region defined by the cooling header from the start of the cooling zone to the zone outlet and the width of the cooling header.

  According to the present invention, in the cooling zone in the vertical continuous annealing furnace that continuously anneals while transporting the strip in the vertical direction, the water contained in the mist sprayed on the strip dripped down the surface of the strip. The occurrence of temperature unevenness in the width direction of the strip can be suppressed, and thereby, for example, a cold-rolled high-tensile material with good flatness can be stably manufactured.

The best mode for carrying out the present invention will be described below in detail with reference to the accompanying drawings.
FIG. 1 is an explanatory view schematically showing a configuration of a test apparatus 1 for a strip type continuous annealing furnace used in the present embodiment.

  In this continuous annealing furnace test apparatus 1 (hereinafter referred to as “continuous annealing furnace 1”), the strip 3 of the cold-rolled steel sheet unwound from the winding coil 2 is successively and continuously directed horizontally and downward. While being conveyed, the electric heating furnace 4 is statically heated to a predetermined temperature and then soaked for about 2 minutes. The electric heating furnace 4 has the ability to heat and slowly cool a steel plate having a length of 1.5 m and a width of 500 mm to 850 ° C., and the temperature pattern of heating can be freely controlled.

  The strip 3 heated by the electric heating furnace 4 passes through the seal roll 5 and is guided to the first cooling zone 6. The seal roll 5 prevents spray water from blowing up from the first cooling zone 6 toward the electric heating furnace 4.

  In the first cooling zone 6, the strip 3 is cooled by being sprayed with a mist (or water-only spray) in which water and gas are mixed from a first air / water nozzle (not shown) while being conveyed downward. To the support roll 7.

  Although not shown, a first water knife as a water nozzle is disposed between the first cooling zone 6 and the support roll 7 and immediately below the first cooling zone 6, and this By spraying from the first water knife toward the surface of the strip 3 that has passed through the first cooling zone 6, it is possible to drain the dripping water on the surface of the strip 3. It is desirable to suppress the occurrence of unevenness.

  The strip 3 passes through the support roll 7 that rotates in contact with the surface of the strip 3 and is prevented from flickering and scratching. The strip 3 is then sent to the second cooling zone 8.

  The strip 3 is cooled by being sprayed with a mist mixed with water and gas from a second air-water nozzle (not shown) while being conveyed downward in the second cooling zone 8. As described above, in the continuous annealing furnace 1, the mist is sprayed toward the surface of the strip 3 by the cooling zone 9 including the first cooling zone 6 and the second cooling zone 8 to cool to a predetermined temperature. Heat treatment. In this way, the desired mechanical properties are imparted to the strip 3.

  The strip 3 that has passed through the second cooling zone is sent to the inspection table 11 via the deflour 10. The flatness of the strip 3 on the inspection table 11 is measured by scanning with a laser displacement meter.

  Although not shown, a second water knife, which is a water nozzle, is arranged between the second cooling zone 8 and the deflor 10 and immediately below the second cooling zone 8. By spraying from the two water knives toward the surface of the strip 3 that has passed through the second cooling zone 8, it is possible to drain dripping water on the surface of the strip 3, thereby causing uneven temperature in the width direction of the strip 3. It is desirable to suppress the occurrence of

  Further, a gas knife that is a gas jet nozzle is arranged below the second water knife, and dripping water is drained by spraying a draining gas from the gas knife toward the surface of the strip 3, It is desirable to suppress the occurrence of temperature unevenness in the width direction of the strip 3.

  As described above, in the present embodiment, the heating strip 3 continuously conveyed in the vertical direction is used with the cooling zone 9 including the first cooling zone 6 and the second cooling zone 8. A cold-rolled steel sheet is produced by continuously cooling and heat-treating the strip 3 by spraying mist containing water.

  When producing a cold-rolled steel sheet by continuously heat-treating the strip 3 in this way, when the temperature of the strip 3 is more than 400 ° C, the temperature of water contained in the mist is 45 ° C or less, When the temperature of the strip 3 is 400 ° C. or lower and 200 ° C. or higher, the temperature of water contained in the mist is set to 40 ° C. or higher. Hereinafter, the reason for limiting the temperature of the water contained in the mist according to the temperature of the strip 3 will be described.

FIG. 2 is an explanatory view schematically showing the configuration of the test apparatus 20 for cooling the test piece 22 of the strip that is fixedly held.
In this test apparatus 20, a 600 mm-wide cooling spray is sprayed on the surface of a test piece 22 (high-tensile cold-rolled steel sheet having a thickness of 1.4 mm, a width of 300 mm, and a length of 300 mm) fixedly supported by a fixing jig 21. The first air / water cooling header 23 and the second air / water cooling header 24 are arranged, and the test piece 22 and the first air / water cooling header 23 and the second air / water cooling header 24 are manually operated. A shutter 25 (a steel plate having a thickness of 1.0 mm, a width of 500 mm, and a length of 500 mm) is disposed, and a thermocouple 26 and a recorder 27 for recording the surface temperature of the test piece 22 are disposed.

  Then, while changing the amount of cooling water contained in the mist sprayed from the first air-water cooling header 23 and the second air-water cooling header 24, the temperature of the test piece 22 and the temperature of the test piece 22 in various ways, By opening and closing, the mist was sprayed on the surface of the test piece 22 to cool the test piece 22, and a basic test for measuring temperature unevenness generated in the test piece 22 was performed. From the results of this basic test, items (a) to (c) listed below were found.

(A) When the amount of water contained in the mist is increased in order to increase the cooling rate of the test piece 22, the width direction deviation of the width direction water amount distribution increases, and the temperature unevenness generated in the test piece 22 increases. This is considered to be due to partial excessive cooling mainly due to dripping water flowing down the surface of the test piece 22.

  FIG. 3 shows a strip 3 heated to 800 ° C. (plate thickness 1.1 mm, width 500 mm) using the continuous annealing furnace 1 shown in FIG. 1 while being transported downward at a transport speed of 30 m / min. It is a graph which shows the influence of the amount of cooling water which has on the temperature irregularity which generate | occur | produced in the width direction of the strip 3 at the time of spraying the mist which changed the quantity of the cooling water with the cooling zone 9, and cooling to 300 degreeC.

  As shown in the graph in the figure, it can be seen that when the amount of water contained in the mist is increased, the temperature unevenness generated in the plate width direction of the test piece 22 increases substantially linearly.

(B) FIG. 4 is a graph showing the influence of water temperature on the cooling ability of mist. As shown in the graph in the figure, it can be seen that when the temperature of the water contained in the mist is lowered, the cooling ability of the mist increases by about 2.5% per 1 ° C. Therefore, when the temperature of this water is lowered by 40 ° C. from 60 ° C. to 20 ° C., the mist cooling capacity can be doubled without increasing the amount of water. Since only the temperature of the water contained in the mist is lowered and the amount of water itself does not increase at all, the temperature unevenness in the width direction does not increase.

(C) FIG. 5 shows the cooling water temperature and water density (actual machine) which affect the quench starting point steel plate temperature (° C.), which is the transition temperature (quenching starting point temperature) for transition from film boiling to nucleate boiling in this basic test. It is a graph which shows the relationship with 800, 500, 200 m < ³ > / h) by total water quantity.

As understood from the graphs shown in FIGS. 4 and 5, the quench start point temperature and the cooling capacity (cooling rate) vary depending on the water temperature and the water density. In general, the cooling capacity (heat transfer coefficient) is proportional to the power density of 0.6. Here, as shown in the graph of FIG. 5, actual equivalent 500 meters ³ / h water distribution total water of ± 60% about variation in actual equivalent in the plate width direction based on the (200～500～800M in actual equivalent ³ / h) Further, if the water temperature is changed by 30 to 70 ° C., it can be seen that the quench starting point temperature varies in the range of about 260 to 400 ° C. That is, the quench start point temperature is proportional to the water density of about 0.1 to 0.2 and does not change much, but the cooling rate (exactly the surface heat transfer coefficient) is proportional to the water density of 0.6. Therefore, if the water amount distribution fluctuates ± 60% in the plate width direction, the cooling rate fluctuates from 58% to 133%. In the two cooling zones, the target cooling amount is 450 ° C. → 250 ° C. (ΔT = 200 ° C.), but the stop temperature fluctuation is 184 ° C. to 334 ° C. (temperature unevenness about 150 ° C.) in the width direction (ΔT fluctuation = 116 to 266 ° C.). Occurs.

  Until now, the cooling capacity has been controlled by changing the amount of water. However, when the amount of water is increased, the deviation of the water amount distribution and drooping water increase, and the temperature unevenness of the strip 3 is likely to occur. Furthermore, in the place where the water density in the strip 3 is large, the temperature is partially lowered, quenching occurs, and the temperature unevenness further increases. That is, when a cooling region in which the quench start point temperature is sandwiched in the cooling zone (particularly in the strip width direction) is generated at the stage where the strip 3 is being cooled, temperature unevenness in the plate width direction increases. For this reason, in order to prevent this increase in temperature unevenness, it is important not to generate the quench start point temperature in the cooling zone.

  Here, when the cooling capacity is controlled by changing the temperature of the water, as shown in the graph of FIG. 5, the water density does not change. Cooling and quenching are less likely to occur, and uniform cooling can be performed.

However, even when the cooling capacity is controlled by changing the temperature of the water, if cooling is performed with water having a low temperature in the zone where the temperature of the strip 3 is decreased, the cooling stop temperature is deteriorated because it is easy to quench. To do. For example, in the example shown in the graph of FIG. 5, when the temperature of the test piece 22 is as low as 300 ° C. or lower, low-temperature water (40 ° C., Qw 800 to 500 m ³ / h equivalent to the actual water amount (80% to 50% of the actual water amount). %)), Quenching occurs, and film boiling shifts to transition / nuclear boiling, thereby increasing the temperature unevenness of the test piece 22 in the width direction.

  Therefore, in the present invention, the first half of the cooling zone in which the temperature of the strip 3 is high performs cooling with water at a low temperature to perform sufficient strong cooling, and conversely in the second half of the cooling zone in which the temperature of the strip 3 is low. Cooling by raising the water temperature lowers the quench starting point temperature to make it difficult to quench, thereby preventing partial rapid cooling.

  Specifically, in this embodiment, the water contained in the mist sprayed on the strip 3 in the cooling zone 9 of the continuous annealing furnace 1 for continuously passing the strip 3 heated and held at a predetermined temperature. Temperature,

(I) In the first cooling zone 6 in which the temperature of the strip 3 is higher than 400 ° C., the amount of water contained in the mist is not increased by setting the temperature to 45 ° C. or less. Without enough cooling of the strip 3,

(Ii) In the second cooling zone 8 in the vicinity of the quench start point temperature at which the cooling rate rapidly changes, that is, the temperature of the strip 3 is 400 ° C. or lower and 200 ° C. or higher, the temperature is set to 40 ° C. or higher (the amount of water is 500 L / Min / m ² or less to reduce the temperature from the quench point temperature to the stop temperature to prevent an increase in temperature unevenness), to reduce the quench start point as much as possible and avoid the temperature unevenness (250 ° C.) When cooling to normal, normal quenching occurs, but the temperature unevenness can be reduced by making the generated temperature as close to the stop temperature as possible), so that the uneven temperature in the width direction of the strip 3 can be substantially eliminated. As a result, a cold-rolled steel sheet with good flatness can be finally produced.

  In the present embodiment, the temperature of the water contained in the mist sprayed on the strip 3 is controlled. However, the temperature of the gas contained in the mist may also be controlled.

  That is, in the continuous annealing furnace 1 in which the heated and soaked strip 3 is continuously passed, in the cooling zone 9 for cooling the strip 3 by spraying mist mixed with water and gas, (i) the cooling zone In the first cooling zone 6 in which the temperature of the strip 3 is in the region where the temperature of the strip 3 exceeds 400 ° C. from the preceding stage to the middle stage of FIG. 9, the temperature of the water contained in the mist is set to 45 ° C. or less. In the second cooling zone 8 in which the temperature of the strip 3 is 400 ° C. or lower and 200 ° C. or higher from the second stage to the latter stage, the temperature of the water contained in the mist is set to 40 ° C. or higher. As a result, in the first cooling zone 6, sufficient cooling can be performed while suppressing the occurrence of temperature unevenness in the width direction of the strip 3 due to dripping water in the strip 3, and in the second cooling zone 8, Cooling can be performed while suppressing the occurrence of temperature unevenness in the width direction of the strip 3 due to the transition from film boiling to nucleate boiling. Together, the occurrence of temperature unevenness in the width direction of the strip 3 can be suppressed, so that a cold-rolled steel sheet having good flatness and predetermined mechanical properties can be manufactured reliably and inexpensively.

  From such a viewpoint, the lower limit of the temperature of the water contained in the mist in the first cooling zone 6 where the temperature of the strip 3 is in the region of more than 400 ° C., and the temperature of the strip 3 is 400 ° C. or less and 200 ° C. or more. The upper limit of the temperature of the water contained in the mist in the second cooling zone 8 that is the region is not necessarily limited, but if the temperature of the water in the second cooling zone 8 becomes too high, It is desirable that the temperature be 70 ° C. or lower because a film is easily generated and the cooling capacity is lowered. Moreover, when the temperature of the water in the 1st cooling zone 6 becomes low too much, a cooling capability will rise and it will become easy to generate | occur | produce the deformation | transformation of the steel plate by rapid cooling, Therefore It is desirable that it is 20 degreeC or more.

  In order to control the temperature of the water contained in the mist as described above, various means commonly used for controlling the temperature of the supplied water may be used, and the specific means is not limited. For example, in the first cooling zone 6 and the second cooling zone 8 in the continuous annealing furnace 1 shown in FIG. 1 described above, the temperature of water is controlled for each unit in which each cooling header or a plurality of headers are collected. Adding equipment (for example, a heat exchanger, a clean water supply system, etc.) is exemplified.

Moreover, in this Embodiment, since the temperature of the water in the 2nd cooling zone 8 is set to the appropriate temperature of 40 degreeC or more, in other words, water temperature control can be performed and the cooling capacity of the whole cooling zone 9 can be improved. The total amount of water in the second cooling zone 8 can be made constant or reduced. For this reason, for example, high-strength materials such as high-tensile materials can be appropriately cooled (cooled to a low temperature, for example, 300 ° C. or lower at a certain cooling rate). Specifically, the total amount of water contained in the mist sprayed on the strip 3 is equal to or less than a predetermined value, for example, 500 (L / m ² ) / min or less, preferably 500 in terms of the average water density at the water jet collision point. It is desirable to reduce to (L / m ² ) / min or less and 50 (L / m ² ) / min or more.

  Thus, according to the present embodiment, the desired strength can be ensured even if the content of the alloy element is reduced in proportion to the amount that can be properly cooled, and the cooling stop temperature is further reduced. A cold-rolled steel sheet with good flatness and no performance variation in the width direction can be produced.

Furthermore, the present invention will be described more specifically with reference to examples.
Using a continuous annealing furnace for actual production having the same configuration as the continuous annealing furnace 1 shown in FIG. 1, heat treatment was performed on the strip 3 made of a high-tensile material to produce a cold-rolled steel sheet having a tensile strength of 980 MPa. The test results are summarized in Table 1 together with the test conditions.

  In Conventional Example 1 in Table 1, the amount of water was 100% in both the first cooling zone 6 and the second cooling zone 8, and the water temperature was 55 ° C. Moreover, in order to ensure the strength of the cold-rolled steel sheet, a material added with an alloy element was used as a base material. In Conventional Example 1, the amount of dripping water was large and the temperature unevenness in the width direction of the strip 3 was 55 ° C. As a result, poor flatness (ear wave) occurred.

  In Conventional Example 2 in Table 1, the amount of water in the first cooling zone 6 is 85% and the amount of water in the second cooling zone 8 is 70%. In addition, the water temperature was lowered to 50 ° C. slightly from that of Conventional Example 1. In Conventional Example 2, the amount of dripping water decreased, the temperature unevenness in the width direction of the strip 3 decreased to 30 ° C., and the flatness defect decreased. However, since the cooling was insufficient and the cooling stop temperature was 270 ° C., which was higher than the target 250 ° C., the effect of increasing the strength by water cooling was insufficient, and it was necessary to add some alloy elements.

  In contrast, in Example 1 of the present invention, the amount of water in the first cooling zone 6 was set to 70% and the amount of water in the second cooling zone 8 was set to 70%. The water temperature was 44 ° C. In Example 1 of the present invention, cooling is stopped even when the amount of water is below a certain level (reduced compared to Conventional Example 2, the amount of water in the first cooling zone 6 is reduced from 85% to 70%, and the amount of water in the second cooling zone 8 is constant). The temperature dropped to the target of 250 ° C., and a sufficient increase in strength became possible. Further, it is not necessary to increase the content of the alloy element of the base material, and the manufacturing cost can be reduced.

  Furthermore, in Invention Example 2, the water temperature in the first cooling zone 6 was reduced to 36 ° C. compared to Invention Example 1. According to Example 2 of the present invention, since the cooling capacity can be afforded, the conveyance speed can be increased to 90 m / min, which is the same as the conventional one, and the productivity is improved, which is very advantageous.

  That is, in Examples 1 and 2 of the present invention, the temperature of the strip 3 is 400 ° C. or higher in the first cooling zone 6, and the water temperature is set to 45 ° C. or lower to obtain sufficient cooling capacity to sufficiently cool the second cooling zone 8. Then, since the plate temperature is 400 to 200 ° C., which is in the vicinity of the quench start point where the shape is easily broken, by setting the water temperature as high as 40 ° C. or higher, the quench start point is avoided as much as possible to perform cooling without increasing the temperature unevenness.

  As a result, the temperature unevenness in the width direction of the strip 3 was reduced by half, and the stop temperature could be lowered to 250 ° C. Therefore, there was no material variation based on an inexpensive base material with a small content of alloy elements, and the flatness was good. New cold-rolled steel sheets can be manufactured.

  In the comparative example in Table 1, the temperature of water in the second cooling zone is 37 ° C., which is lower than the range specified in the present invention, but the temperature unevenness in the plate width direction is as large as 83 ° C. Occurred and the flatness of the cold-rolled steel sheet was unsatisfactory.

  Thus, according to Invention Examples 1 and 2, compared to Conventional Examples 1 and 2, a desired high-strength cold-rolled steel sheet is produced even when an inexpensive base material having a low alloy element content is used. In addition, since the productivity can be secured at a high level, a cold-rolled steel sheet with little variation in the mechanical properties in the width direction and good flatness can be produced at low cost.

It is explanatory drawing which shows typically the structure of the test apparatus of the continuous annealing furnace of the strip used by embodiment. It is explanatory drawing which shows typically the structure of the test apparatus for cooling the test piece of the strip fixedly held. Using the continuous annealing furnace shown in FIG. 1, while the strip heated to 800 ° C. is conveyed downward at a conveyance speed of 30 m / min, mist with various amounts of cooling water is sprayed by the cooling zone. 6 is a graph showing the influence of the amount of cooling water on the temperature unevenness generated in the width direction of the strip when cooled to 300 ° C. It is a graph which shows the influence of the temperature of water on the cooling capacity of mist. In the basic test, the temperature of the cooling water, the water density (800, 500 corresponding to the total water volume of the actual machine), which influences the quench starting point steel plate temperature (° C.) which is the transition temperature (quenching starting point temperature) transitioning from film boiling to nucleate boiling. It is a graph which shows a relationship with 200m < ³ > / h).

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Test apparatus of continuous annealing furnace 2 Unwinding coil 3 Strip 4 Electric heating furnace 5 Seal roll 6 1st cooling zone 7 Support roll 8 2nd cooling zone 9 Cooling zone 10 Deflor 11 Inspection table

Claims (2)

  When manufacturing a cold-rolled steel sheet by continuously cooling and heat-treating the strip by continuously spraying the mist containing water or water on the heated strip that is continuously conveyed in the vertical direction, When the temperature of the strip exceeds 400 ° C., the temperature of the water is 45 ° C. or lower, and when the temperature of the strip is 400 ° C. or lower and 200 ° C. or higher, the temperature of the water is 40 ° C. or higher. A method for producing a cold-rolled steel sheet. The method for producing a cold-rolled steel sheet according to claim 1, wherein the total amount of water sprayed on the strip is 500 (L / m ² ) / min or less in terms of an average water density at the water jet collision point.

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